CN1074047C - Method for using coal fines in a melt-down gasifier - Google Patents
Method for using coal fines in a melt-down gasifier Download PDFInfo
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- CN1074047C CN1074047C CN98806792A CN98806792A CN1074047C CN 1074047 C CN1074047 C CN 1074047C CN 98806792 A CN98806792 A CN 98806792A CN 98806792 A CN98806792 A CN 98806792A CN 1074047 C CN1074047 C CN 1074047C
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- accordance
- ickings
- gasification furnace
- coal dust
- melting gasification
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/0006—Making spongy iron or liquid steel, by direct processes obtaining iron or steel in a molten state
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
- C10L5/10—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders
- C10L5/14—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders with organic binders
- C10L5/16—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders with organic binders with bituminous binders, e.g. tar, pitch
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/361—Briquettes
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/0006—Making spongy iron or liquid steel, by direct processes obtaining iron or steel in a molten state
- C21B13/0013—Making spongy iron or liquid steel, by direct processes obtaining iron or steel in a molten state introduction of iron oxide into a bath of molten iron containing a carbon reductant
- C21B13/002—Reduction of iron ores by passing through a heated column of carbon
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/0066—Preliminary conditioning of the solid carbonaceous reductant
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/14—Multi-stage processes processes carried out in different vessels or furnaces
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Metallurgy (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Geology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Manufacture Of Iron (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
In a method for the production of liquid metal, in particular liquid pig iron ( 9 ) or liquid steel pre-products, from metal carriers, in particular partially reduced or reduced sponge iron ( 3 ), in a melter gasifier ( 1 ) in which with supply of a carbon-containing material at least partially formed of fine coal ( 16 ) and coal dust ( 13 ) and with supply of oxygen or oxygen-containing gas the metal carriers are melted in a bed ( 4 ) of the carbon-containing material at the simultaneous formation of a reducing gas, optionally upon previous final reduction, fine coal ( 16 ) and coal dust ( 13 ) which are being charged, are mixed with bitumen ( 20 ) in the hot state, after undergoing a drying operation, and subsequently are cold-briquetted, and the briquettes ( 25 ) thus formed are charged to the melter gasifier ( 1 ) in the cold state and in the melter gasifier ( 1 ) are subjected to shock-heating.
Description
The present invention relates in melting gasification furnace (Einschmelzvergaser), produce liquid metal especially liquid pig iron or liquid steel process of semi-finished by metallic carrier especially partial reduction or reductive sponge iron, in melting gasification furnace by infeeding material containing carbon and oxygen or the oxygen containing gas that constitutes by ickings and coal dust to small part, metallic carrier is in the bed that is made of carbonaceous material, when generating reducing gas, in case of necessity in final reduction back melting in advance.The invention still further relates to the equipment of implementing this method.
The problem that exists when infeeding particulate carbon-containing material such as ickings and coal dust in melting gasification furnace is, because the speed that exists in melting gasification furnace is discharged the particulate carbon-containing material again from melting gasification furnace.This situation also is applicable to particulate ore on same degree.In order to address the above problem, for example advise in AT-B-401777 that the carrier of carbon adds in the melting gasification furnace by means of pulverised fuel burner with ore deposit bits and/or breeze, and adds in the lower region of melting gasification furnace.The carbon support that here causes adding is lower than the burning by stoichiometry.The shortcoming of bringing is that the carrier of carbon can not be made contributions for set up the bed that is made of the solid carbon support in melting gasification furnace.
Knownly in inside infeed microgranular coal to the melting gasification furnace upper zone, microgranular coal transforms coking therein, burntly discharge and separate with reducing gas, then with particulate material by burner input melting gasification furnace.Yet here for setting up the same not contribution of the bed that constitutes by carbonaceous material.
This bed is made of the lumped coal that must have high thermostability usually.Based on the development of the coal market about the needs that are subjected to the coal-burning power plant, the situation of coal dust may take place preferably to provide, be used for popular coal burner nowadays.Original grate firing that must use lump coal commonly used only plays accessory effect now on the consumption market of coal.Consequently, the fine fraction of the coal of supplying on market may account for very big ratio, and its order of magnitude changes in 50 to 70% scope.
When in melting gasification furnace, using this coal, at first the fine fraction of coal is sifted out usually, have only coarse fraction, that is lumped coal, just be provided for melting gasification furnace.Fine fraction is for other local use.
The objective of the invention is, fine fraction is used equally valuably, make it help to set up the bed that constitutes by carbonaceous material in the melting gasification furnace, can reduce the cost that uses bulk carbonaceous material thus.
By the present invention is to reach the measure that this purpose takes to be, ickings that add and coal dust are hot after drying to be mixed with pitch earth down, follows cold briquetting; And the agglomerate of making thus adds melting gasification furnace in cold conditions, and is subjected to heating sharp in melting gasification furnace.
Find that unexpectedly the agglomerate of so making has fabulous thermostability, it in addition surpass the thermostability of blocky carbonaceous material.Under the impact type effect of the about 1000 ℃ temperature of melting gasification furnace, small avalanche phenomenon only appears in agglomerate.This will be owing to the asphaltic character as binding agent, and pitch earth is in quick fusing under the above-mentioned high temperature and thereby for the condition that provides advantageously is provided between the coal grain.Here importantly, pitch earth can bubbing under said temperature and is kept its heavy-gravity denseness and bounding force in addition.
The briquet that constitutes by a kind of mixture by the known use of DE-A-2407780, this mixture comprises as the selected fine of now using coal especially hard coal and/or meager coal or coal dust and as the high vacuum pitch earth of binding agent, the agglomerate of so making is used for for example in family expenses burner internal combustion, or perhaps can be used for blast furnace, as long as they are able to take a kind of thermal processing, as oxidation, carbonization at low temperature or coking.Yet this agglomerate satisfies is the different requirement that will satisfy with agglomerate by manufacturing of the present invention, especially by thermostability importantly in the agglomerate of the present invention, that is to say, agglomerate should not burst when being subjected to unexpected thermal shocking when adding as furnace charge in the melting gasification furnace, and by DE-A-2407780 importantly agglomerate high stability is arranged, just high bearing capacity to be arranged, so that can in blast furnace, use.By known method, the high vacuum pitch earth is heated to 200 ℃, and is mixing back briquetting under about 85 ℃ temperature with coal dust.Because most of coking in known agglomerate is so produce high stability.
According to a kind of best form of implementation, ickings and coal dust are separated from the carbonaceous material that adds as furnace charge when drying and/or after dry and are further handled down hot.
Produced simultaneously bulk carbonaceous material when separating ickings and coal dust is by a kind of preferred implementing form of the present invention, in the melting gasification furnace of directly packing into.
Granularity is preferably separated from material containing carbon smaller or equal to the ickings of 8mm.
By the method for the described type of the known a kind of preface of EP-B-0315825, wherein, ickings grinds back and binding agent, and for example lime, molasses, pitch or tar mix and granulating, then add in the melting gasification furnace.By of course not granulation but briquetting of the present invention, comparing agglomerate with granular solid has higher thermo mechanical stability.By another shortcoming of EP-B-0315825 is that to be used to grind the needed energy consumption of ickings big.Then avoided this shortcoming by the present invention,, but isolated ickings and coal dust because the carbonaceous material of packing into as furnace charge need not to grind.
By the known a kind of method of AT-B-376241, according to said method, from reducing gas, separate and sintering from the solid of forming by powdery carbon that melting gasification furnace is discharged with reducing gas, and formed agglomerate especially formed coke sent back in the melting gasification furnace, yet here, as by the present invention, the carbonaceous material that adds as furnace charge does not carry out sintering and can not obtain larger-size ickings adding as furnace charge.Also have a shortcoming to be in by the method for AT-B-376241, agglomerating plant is directly arranged in the back of the hot cyclone separator that is used to separate powdery carbon, thereby causes expensive construction expenditure.
Ickings or the coal dust separated from the carbonaceous material that adds as furnace charge by the present invention mix also briquetting with pitch earth, the briquetting device is located at the downstream of carbonaceous material drying installation in this case.Conform with purpose here be with pitch earth mixing process in and make full use of dry back ickings and the contained heat of coal dust during in briquetting.For briquetting need not to use any additional heat energy.
Optimum design according to said method, ickings and coal dust and pitch earth are lower than 100 ℃ in temperature, preferably temperature 75 with 80 ℃ between the time mix.Advantageously add softening temperature and be lower than 80 ℃ of pitch earth that are preferably lower than 75 ℃.
Infeed additional heat in mixing process in case of necessity, asphaltic softening to guarantee.
By a kind of preferred form of implementation of the inventive method, be added to 30% petroleum coke as material containing carbon, itself does not have enough thermostabilitys.But still have enough high thermostabilitys by means of the agglomerate that obtains by process of the present invention.
The carbonaceous material that adds as furnace charge preferably is dried to residual moisture content and is lower than 5%.
According to a kind of embodiment, broken agglomerate is separated from the agglomerate that is made of ickings and coal dust and recirculation in the briquetting process.
When the agglomerate that is made of ickings and coal dust is preferably in briquetting and/or the briquetting postcooling be lower than 30 ℃ to temperature.They have extra high thermostability, when especially being subjected to heat sharp in adding melting gasification furnace.
By the present invention, preferably using ash content is 10 to 25% coal.Therefore the characteristics by method of the present invention are extra high economy, so in melting gasification furnace, produce also marked downly by the liquid metal of partially or completely reductive metallic ore melting, because the carbonaceous material that is used to make agglomerate just that has added for melting gasification furnace as foreword has illustrated, these agglomerates are the so-called byproducts that utilize the particulate of carbonaceous material partly to obtain.
Also can use the coal of volatilization composition between 18 and 38% by the present invention.That is to say and there is no need to use fat coal.
Preferably have temperature when coal dryer is discharged and ickings and coal dust and mix, want the temperature of blended material when mixing to be preferably 70 to the highest 100 ℃, especially 75 to 85 ℃ in this case with the pitch earth that this uniform temp is arranged substantially.Guarantee bond effect that pitch earth is good and cheap temperature control thus.In addition, the mixed product of being made up of ickings, coal dust and pitch earth need not cooling or only cooling slightly before its briquetting.
Can think by another advantage of the inventive method to be, can use pitch earth that the locality is generally used for paving the way here as required pitch earth.That is to say and there is no need pitch earth is proposed special requirement.
The equipment that enforcement is used by method of the present invention comprises melting gasification furnace; Feed the metallic carrier input tube of partial reduction or reducing sponge iron especially in the melting gasification furnace; The input tube of oxygen or oxygen-containing gas and the carbonaceous material that constitutes by ickings and coal dust to small part; The vent pipe of the reducing gas that in melting gasification furnace, generates of drawing from melting gasification furnace; And be located at the pig iron on the melting gasification furnace and the iron notch or the slag notch of slag, it is characterized in that, an if moisture eliminator, be used for the dry carbonaceous material that adds as furnace charge, the cold briquetting device that is used for ickings and coal dust briquetting of establishing stirrer in its downstream and being attached thereto, wherein, cold briquetting device couples together with melting gasification furnace on pipeline.
According to a kind of preferred form of implementation, be provided with separator, be used for ickings and coal dust are separated from the carbonaceous material that adds as furnace charge.
According to the preferred form of implementation of another kind, the input tube that is used to add bulk carbonaceous material is directly arranged in the melting gasification furnace.
For the heated and stirred machine is preferably established a vapour generator.
Be preferably in and establish a device that is used to separate broken agglomerate between cold briquetting device and the melting gasification furnace.
Further specify the present invention by means of accompanying drawing below, accompanying drawing illustrates a kind of preferred form of implementation of the present invention.
Represent melting gasification furnace with 1 in the drawings, be added to small part reductive sponge iron 3 by input tube 2, sponge iron is melting after final reduction in case of necessity in melting gasification furnace 1, or rather melting in the process of passing the bed 4 that is made of carbonaceous material.Reducing gas vent pipe 7 and the fused pig iron 9 and slag fused 10 outlet 8,8a separately that melting gasification furnace 1 also is equipped with the input tube 5, carbonaceous material input tube 6a, 6b of aerobic or oxygen-containing gas, generates in melting gasification furnace 1.
The carbonaceous material 11 that adds as furnace charge is at first moisture eliminator, 12 inner dryings.Produced simultaneously here coal dust 13 is discharged from and further handles in second moisture eliminator 14.Have an appointment 60 ℃ temperature of the carbonaceous material of the heat of discharging from first moisture eliminator 12, it is transfused to separator 15, for example is a sieve, and ickings 16 separates with blocky carbonaceous material 17 there.For example having granularity is separated smaller or equal to the ickings 16 of 8mm.
Bulk carbonaceous material 17 directly adds melting gasification furnace 1 through input tube 6b.16 differences of ickings, it enters storage tank 18 and removes stirrer 19 more therefrom, and ickings 16 mixes with pitch earth 20 in stirrer, and pitch earth is then from pitch earth case 21.Also import stirrer 19 from the coal dust 13 of second moisture eliminator 14, it is relay storage in coal dust pot 22.
Stirrer 19 arrives about 75-80 ℃ by means of the steam heating that vapour generator 23 produces.Guarantee to surpass the softening temperature of the pitch earth of importing 20 thus.But heat content that also might ickings 16 has been enough to be provided as the required heat energy of softening pitch earth 20, therefore need not to re-use to be any additional energy of steam for this reason in form.
The pitch earth of being adopted 20 can be to have softening temperature to be lower than 75 ℃ the common petroleum pitch that is used to pave the way, and it can cheapness provide everywhere in the whole world, and for example the pitch earth by the kind B70 of NORM B3610 has following technical qualification:
Softening temperature, ring and ball ( NORM C9212): 47-54 ℃
Pin in the time of 25 ℃ is worn ( NORM C9214): 50-80mm * 10
-1
Follow by means of the cold briquetting under about 70 to the 75 ℃ situation of temperature of cold briquetting device 24 by the mixture that ickings 16, coal dust 13 and pitch earth 20 are formed, that is to say, for any additional heat energy is not used in briquetting.The agglomerate 25 last input units of so making 26, so that will not have for using the broken agglomerate of the size that requires to separate in melting gasification furnace 1, this device 26 is simultaneously as refrigerating unit.Agglomerate 25 is cooled to temperature here and is lower than 30 ℃.
Do not have in melting gasification furnace 1, using broken agglomerate recirculation in the briquetting process of the size that requires.They at first enter collector 27, again the storage tank 18 from entering ickings 16 here.
Agglomerate 25 infeeds melting gasification furnace 1 through input tube 6a, and they stand rapid heating therein.Find that unexpectedly this agglomerate 25 has high thermostability, even higher than the thermostability of bulk carbonaceous material 17, for example this point can be described by means of following.
By method drying of the present invention and screening South Africa and Australian bituminous coal, obtain the fraction of lumped coal and coal dust and ickings here.Coal dust and ickings adopt by briquetting method of the present invention briquetting.Then relatively with the thermostability of the thermostability of the agglomerate that so makes and relevant lumped coal.
Determine thermostability by such method, that is, be that a fraction of 10 to 16mm is heat-treated with the granularity of using that has, and after thermal treatment, sieve.Granularity surpasses part that 10mm or granularity be lower than 2mm and weighs respectively and provide the per-cent that accounts for usage quantity.Table 1 combines the result of gained.
Table 1
| South Africa bituminous coal | Australia's bituminous coal | |||
| The coal that uses | Agglomerate | The coal that uses | Agglomerate | |
| Thermostability+10mm%-2mm% | 77.6 3.1 | 86.4 2.6 | 77.7 3.4 | 82.4 2.4 |
It is high more and granularity is more little less than the ratio of 2mm that granularity surpasses the ratio of 10mm, and then thermostability is high more.Can obviously find out by table 1, by means of its thermostability of the agglomerate of making by method of the present invention apparently higher than relevant lumped coal.
Therefore, employing provides the agglomerate of being made up of ickings and coal dust of use to have high thermostability by program of the present invention, so they can use in melting gasification furnace immediately, even under the impact type effect of the about 1000 ℃ temperature of melting gasification furnace, the avalanche phenomenon of agglomerate also seldom.Therefore succeed in doing with economic mode and in melting gasification furnace, use ickings and coal dust, exactly in such a way, promptly, the agglomerate of being made by ickings and coal dust helps to set up the bed that a carrier by carbon constitutes in melting gasification furnace, can significantly reduce the cost that uses bulk carbonaceous material thus.
Claims (26)
1. in melting gasification furnace (1), produce the method for liquid metal by metallic carrier, in melting gasification furnace by infeeding material containing carbon and oxygen or the oxygen containing gas that constitutes by ickings (16) and coal dust (13) to small part, metallic carrier is in the bed (4) that is made of material containing carbon, melting when generating reducing gas, it is characterized by: the ickings (16) and the coal dust (13) that infeed as furnace charge, hotly after drying mix down, follow cold briquetting with pitch earth (20); And, pack in the melting gasification furnace (1) here under the agglomerate of making (25) cold conditions and in melting gasification furnace (1), be subjected to heating sharp.
2. it is characterized by in accordance with the method for claim 1: described metallic carrier is partial reduction or reductive sponge iron (3).
3. in accordance with the method for claim 1, it is characterized by: after final reduction in advance, smelting metal carrier in the bed (4) that constitutes by material containing carbon.
4. it is characterized by in accordance with the method for claim 1: described liquid metal is liquid pig iron (9) or liquid steel work in-process.
5. it is characterized by in accordance with the method for claim 1: ickings (16) and coal dust (13) are separated from infeed the carbonaceous material (11) as furnace charge when drying and/or after dry and are handled hot the continuation down.
6. it is characterized by in accordance with the method for claim 5: produced simultaneously bulk carbonaceous material (17) is directly packed in the melting gasification furnace (1) when separating ickings (16) and coal dust (13).
7. according to claim 5 or 6 described methods, it is characterized by: granularity is separated from material containing carbon smaller or equal to the ickings (16) of 8mm.
8. it is characterized by in accordance with the method for claim 1: ickings (16) and coal dust (13) mix when temperature is lower than 100 ℃ with pitch earth (20).
9. it is characterized by in accordance with the method for claim 8: ickings (16) and coal dust (13) mix between 80 ℃ at 75 ℃ in temperature with pitch earth (20).
10. it is characterized by in accordance with the method for claim 1: add softening temperature and be lower than 80 ℃ pitch earth (20).
11. it is characterized by in accordance with the method for claim 9: add softening temperature and be lower than 75 ℃ pitch earth (20).
12. it is characterized by in accordance with the method for claim 1: infeed additional heat in mixing process.
13. it is characterized by in accordance with the method for claim 1: be added to 30% petroleum coke as material containing carbon.
14. it is characterized by in accordance with the method for claim 1: the carbonaceous material that adds as furnace charge is dried to residual moisture content and is lower than 5%.
15. it is characterized by in accordance with the method for claim 1: broken agglomerate is separated and recirculation in the briquetting process from the agglomerate (25) that is made of ickings (16) and coal dust (13).
16. it is characterized by in accordance with the method for claim 1: the agglomerate (25) that constitutes by ickings (16) and coal dust (13) when briquetting and/or the briquetting postcooling be lower than 30 ℃ to temperature.
17. it is characterized by in accordance with the method for claim 1: the use ash content is 10 to 25% coal (16,13).
18. it is characterized by in accordance with the method for claim 1: use the coal (16,13) of volatilization composition between 18 and 35%.
19. it is characterized by in accordance with the method for claim 1: have that the ickings (16) and the coal dust (13) of temperature mixes with the pitch earth that this same temperature is arranged substantially when coal dryer is discharged.
20. in accordance with the method for claim 19, it is characterized by: the temperature of blended material (13,16,20) when mixing is 70 to the highest 100 ℃, best 75 to 85 ℃.
21. it is characterized by in accordance with the method for claim 1: adopt the local pitch earth that is generally used for paving the way as pitch earth (20).
22. implement equipment, comprise melting gasification furnace (1) according to one of claim 1 to 21 described method; Feed the metallic carrier input tube (2) of partial reduction or reducing sponge iron (3) especially in the melting gasification furnace (1); Oxygen or oxygen-containing gas and to small part by the input tube of the carbonaceous material of ickings (16) and coal dust (13) formation (5,6a, 6b); The vent pipe (7) of the reducing gas that in melting gasification furnace (1), generates of drawing from melting gasification furnace (1); And be located at the iron notch of the pig iron (9) on the melting gasification furnace (1) and slag (10) or slag notch (8,8a), it is characterized by: establish moisture eliminator (12), be used for the dry carbonaceous material (11) that adds as furnace charge, the cold briquetting device (24) that is used for ickings (16) and coal dust (13) briquetting of establishing stirrer (19) in its downstream and being attached thereto, wherein, cold briquetting device (24) couples together with melting gasification furnace (1) on pipeline.
23., it is characterized by: be provided with separator (15), be used for ickings (16) and coal dust (13) are separated from the carbonaceous material (11) that adds as furnace charge according to the described equipment of claim 22.
24. according to claim 22 or 23 described equipment, it is characterized by: the input tube (6b) that is used to add bulk carbonaceous material (17) is directly arranged in the melting gasification furnace (1).
25., it is characterized by: for heated and stirred machine (19) is established a vapour generator (23) according to the described equipment of claim 22.
26., it is characterized by: between cold briquetting device (24) and melting gasification furnace (1), establish a device (26) that is used to separate broken agglomerate according to the described equipment of claim 22.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ATA1157/1997 | 1997-07-04 | ||
| AT0115797A AT407053B (en) | 1997-07-04 | 1997-07-04 | METHOD AND SYSTEM FOR THE PRODUCTION OF A METAL MELT IN A MELTING-UP CARBURETOR USING FINE COAL |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1261923A CN1261923A (en) | 2000-08-02 |
| CN1074047C true CN1074047C (en) | 2001-10-31 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98806792A Expired - Fee Related CN1074047C (en) | 1997-07-04 | 1998-07-03 | Method for using coal fines in a melt-down gasifier |
Country Status (19)
| Country | Link |
|---|---|
| US (1) | US6332911B1 (en) |
| EP (1) | EP1000178B1 (en) |
| JP (1) | JP4184448B2 (en) |
| KR (1) | KR100551608B1 (en) |
| CN (1) | CN1074047C (en) |
| AT (2) | AT407053B (en) |
| AU (1) | AU741816B2 (en) |
| BR (1) | BR9810664A (en) |
| CA (1) | CA2294272C (en) |
| DE (1) | DE59800653D1 (en) |
| MY (1) | MY115594A (en) |
| PL (1) | PL189751B1 (en) |
| RU (1) | RU2188239C2 (en) |
| SK (1) | SK284445B6 (en) |
| TR (1) | TR199903306T2 (en) |
| TW (1) | TW442571B (en) |
| UA (1) | UA53721C2 (en) |
| WO (1) | WO1999001583A1 (en) |
| ZA (1) | ZA985866B (en) |
Families Citing this family (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002090604A2 (en) * | 2001-05-08 | 2002-11-14 | Voest-Alpine Industrieanlagenbau Gmbh & Co. | Method and installation for utilizing waste products, which contain hydrocarbons and iron oxide, particularly mill scale sludges and coal fines |
| KR100584745B1 (en) * | 2001-12-21 | 2006-05-30 | 주식회사 포스코 | Apparatus and method for recycling iron dust and sludge in molten iron manufacturing process using ordinary coal and iron ore |
| CN1852995A (en) * | 2003-12-05 | 2006-10-25 | Posco公司 | An apparatus for manufacturing a molten iron directly using fine or lump coals and fine iron ores, the method thereof, the integrated steel mill using the same and the method thereof |
| AU2004295629B2 (en) * | 2003-12-05 | 2008-11-20 | Posco | An apparatus for manufacturing a molten iron directly using fine or lump coals and fine iron ores, the method thereof, the integrated steel mill using the same and the method thereof |
| UA84305C2 (en) * | 2003-12-05 | 2008-10-10 | Поско | Method and device for obtaining of cast iron melt and hot-rolled steel sheet |
| KR20050077103A (en) * | 2004-01-26 | 2005-08-01 | 주식회사 포스코 | The apparatus for producing molten iron directly using coal with wide range of size and the method using the same |
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- 1998-03-07 UA UA99127249A patent/UA53721C2/en unknown
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- 1998-07-03 RU RU2000102645/02A patent/RU2188239C2/en not_active IP Right Cessation
- 1998-07-03 AT AT98930525T patent/ATE200798T1/en active
- 1998-07-03 DE DE59800653T patent/DE59800653D1/en not_active Expired - Lifetime
- 1998-07-03 JP JP50593999A patent/JP4184448B2/en not_active Expired - Fee Related
- 1998-07-03 BR BR9810664-3A patent/BR9810664A/en not_active IP Right Cessation
- 1998-07-03 EP EP98930525A patent/EP1000178B1/en not_active Expired - Lifetime
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- 1998-07-03 WO PCT/AT1998/000165 patent/WO1999001583A1/en active IP Right Grant
- 1998-07-03 KR KR1019997012599A patent/KR100551608B1/en not_active IP Right Cessation
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- 1998-07-03 PL PL98338039A patent/PL189751B1/en not_active IP Right Cessation
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Also Published As
| Publication number | Publication date |
|---|---|
| SK188799A3 (en) | 2000-07-11 |
| WO1999001583A1 (en) | 1999-01-14 |
| EP1000178B1 (en) | 2001-04-25 |
| TW442571B (en) | 2001-06-23 |
| TR199903306T2 (en) | 2000-07-21 |
| ATA115797A (en) | 2000-04-15 |
| RU2188239C2 (en) | 2002-08-27 |
| UA53721C2 (en) | 2003-02-17 |
| ATE200798T1 (en) | 2001-05-15 |
| BR9810664A (en) | 2000-10-03 |
| JP4184448B2 (en) | 2008-11-19 |
| PL338039A1 (en) | 2000-09-25 |
| CN1261923A (en) | 2000-08-02 |
| CA2294272C (en) | 2004-10-26 |
| JP2002508809A (en) | 2002-03-19 |
| ZA985866B (en) | 1999-01-27 |
| CA2294272A1 (en) | 1999-01-14 |
| AT407053B (en) | 2000-12-27 |
| EP1000178A1 (en) | 2000-05-17 |
| MY115594A (en) | 2003-07-31 |
| SK284445B6 (en) | 2005-04-01 |
| KR100551608B1 (en) | 2006-02-13 |
| AU741816B2 (en) | 2001-12-13 |
| KR20010014415A (en) | 2001-02-26 |
| US6332911B1 (en) | 2001-12-25 |
| AU8091698A (en) | 1999-01-25 |
| DE59800653D1 (en) | 2001-05-31 |
| PL189751B1 (en) | 2005-09-30 |
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